1) The document discusses recent developments in technologies for processing molten aluminum. It outlines the key steps in molten metal processing including crucible pre-treatment, furnace processing, and in-line treatment like degassing and filtration.
2) Recent progress has been made in improving furnace processing technologies like rotary gas injection that increase contact between the metal and fluxing agents, improving impurity removal. However, furnace processing alone cannot achieve the cleanliness required for high-quality products.
3) Ongoing challenges remain in developing simple, accurate, and low-cost on-line tools for assessing metal cleanliness and controlling processing technologies to optimize quality, productivity, costs and environmental impact.
Chemicals used in construction general studies Aditya Sanyal
The document discusses the role of chemicals in the construction industry, focusing on corrosion inhibitors and superplasticizers. It provides an overview of how corrosion inhibitors and superplasticizers improve concrete properties like workability and durability. It also describes CSIR-SERC's research on corrosion inhibitor and superplasticizer performance, including fabric reinforced concrete. The document outlines techniques for evaluating inhibitor efficiency and assessing corrosion in reinforced concrete structures.
This document summarizes a study that investigated how operational parameters influence the bright nickel plating process. The study found that the weight of bright nickel deposited was affected by plating temperature, voltage, current density, pH, and plating time. The best bright nickel deposition was obtained at 56°C, a current density of 6 A/dm2, and a plating time of 18 minutes. The document provides details on the experimental setup and procedures, including the composition of the nickel plating bath and operating conditions that were tested. Results are presented showing correlations between temperature and current density, and the effect of operational parameters on nickel deposition.
This document discusses the electrolytic separation of lead and lead dioxide from roasted carbonate ore residuum. Various electrolyte solutions containing lead ions in simple or complex forms were tested. The optimum conditions for electrolytic extraction were determined experimentally. Cathodic electrodeposition of lead and anodic electrodeposition of lead dioxide were achieved from ore salt baths. Dense, fine-grained lead deposits with high current efficiencies around 95-98% were obtained from complex ore salt solutions like lead silicofluoride, fluoborate, sulphamate, and gluconate baths. Alkaline lead baths also allowed efficient deposition of lead and lead dioxide. Current density, temperature, and metal ion concentration affected the deposition process and current
Cimtec itri pvc eva tin-ldh nanocomposites interflam 2010ITRI Ltd
This document summarizes experimental results from synthesizing and characterizing layered double hydroxide (LDH) nanoparticles and tin-LDH hybrid nanoparticles using different methods. Two LDH synthesis methods were tested: the urea method and NaOH/Na2CO3 method. Characterization using ICP, XRD, SEM and BET surface area analysis showed that the urea method produced well-ordered hexagonal LDH platelets but did not successfully incorporate tin. The NaOH/Na2CO3 method resulted in LDHs and magnesium hydroxy stannate phases with increasing tin content, but platelets were not visible by SEM. The optimal synthesis depends on the desired Mg/Al/Sn ratio and applications require further development
This document reviews copper etching processes using cupric chloride (CuCl2) as the etchant. It discusses how CuCl2 provides a high etch rate and easy regeneration compared to other etchants like ferric chloride. The effects of etchant concentration, additives, and etching temperature on the etch rate are examined. Regeneration processes for waste CuCl2 using chemicals like chlorine gas, hydrogen peroxide, and sodium chlorate are also discussed which allow for recycling of the etchant. Copper etching with CuCl2 is an important process in printed circuit board manufacturing in the electronics industry.
IRJET- Sulphuric Acid Durability Studies of Concrete with Portland Cement (CE...IRJET Journal
This document summarizes a study on the sulphuric acid durability of concrete with different cement types and partial cement replacements. Concrete cubes were made with Portland cement (CEM I), Portland composite cements (CEM II/A-M and CEM II/B-M), and with partial replacements of Portland cement with fly ash and GGBFS. Cubes were submerged in 5% sulphuric acid for 90 days. Results showed concrete with higher Portland cement content was most affected, while CEM II/B-M concrete was most durable. Partial replacements of 25% fly ash and 70% GGBFS showed higher durability against sulphuric acid attack compared to the reference mix.
This document discusses a hydroxylamine-based wet chemistry process for removing photoresist, sidewall polymers, and other residues from plasma processing. It has been found to leave surfaces free of visual contamination. The process exhibits lower levels of mobile ionic contamination than alternatives. The development of sub-micron devices requires clean via holes for low-resistance contacts. Photoresist stripping methods must address issues like mobile ion contamination and plasma damage while simplifying processes.
Chemicals used in construction general studies Aditya Sanyal
The document discusses the role of chemicals in the construction industry, focusing on corrosion inhibitors and superplasticizers. It provides an overview of how corrosion inhibitors and superplasticizers improve concrete properties like workability and durability. It also describes CSIR-SERC's research on corrosion inhibitor and superplasticizer performance, including fabric reinforced concrete. The document outlines techniques for evaluating inhibitor efficiency and assessing corrosion in reinforced concrete structures.
This document summarizes a study that investigated how operational parameters influence the bright nickel plating process. The study found that the weight of bright nickel deposited was affected by plating temperature, voltage, current density, pH, and plating time. The best bright nickel deposition was obtained at 56°C, a current density of 6 A/dm2, and a plating time of 18 minutes. The document provides details on the experimental setup and procedures, including the composition of the nickel plating bath and operating conditions that were tested. Results are presented showing correlations between temperature and current density, and the effect of operational parameters on nickel deposition.
This document discusses the electrolytic separation of lead and lead dioxide from roasted carbonate ore residuum. Various electrolyte solutions containing lead ions in simple or complex forms were tested. The optimum conditions for electrolytic extraction were determined experimentally. Cathodic electrodeposition of lead and anodic electrodeposition of lead dioxide were achieved from ore salt baths. Dense, fine-grained lead deposits with high current efficiencies around 95-98% were obtained from complex ore salt solutions like lead silicofluoride, fluoborate, sulphamate, and gluconate baths. Alkaline lead baths also allowed efficient deposition of lead and lead dioxide. Current density, temperature, and metal ion concentration affected the deposition process and current
Cimtec itri pvc eva tin-ldh nanocomposites interflam 2010ITRI Ltd
This document summarizes experimental results from synthesizing and characterizing layered double hydroxide (LDH) nanoparticles and tin-LDH hybrid nanoparticles using different methods. Two LDH synthesis methods were tested: the urea method and NaOH/Na2CO3 method. Characterization using ICP, XRD, SEM and BET surface area analysis showed that the urea method produced well-ordered hexagonal LDH platelets but did not successfully incorporate tin. The NaOH/Na2CO3 method resulted in LDHs and magnesium hydroxy stannate phases with increasing tin content, but platelets were not visible by SEM. The optimal synthesis depends on the desired Mg/Al/Sn ratio and applications require further development
This document reviews copper etching processes using cupric chloride (CuCl2) as the etchant. It discusses how CuCl2 provides a high etch rate and easy regeneration compared to other etchants like ferric chloride. The effects of etchant concentration, additives, and etching temperature on the etch rate are examined. Regeneration processes for waste CuCl2 using chemicals like chlorine gas, hydrogen peroxide, and sodium chlorate are also discussed which allow for recycling of the etchant. Copper etching with CuCl2 is an important process in printed circuit board manufacturing in the electronics industry.
IRJET- Sulphuric Acid Durability Studies of Concrete with Portland Cement (CE...IRJET Journal
This document summarizes a study on the sulphuric acid durability of concrete with different cement types and partial cement replacements. Concrete cubes were made with Portland cement (CEM I), Portland composite cements (CEM II/A-M and CEM II/B-M), and with partial replacements of Portland cement with fly ash and GGBFS. Cubes were submerged in 5% sulphuric acid for 90 days. Results showed concrete with higher Portland cement content was most affected, while CEM II/B-M concrete was most durable. Partial replacements of 25% fly ash and 70% GGBFS showed higher durability against sulphuric acid attack compared to the reference mix.
This document discusses a hydroxylamine-based wet chemistry process for removing photoresist, sidewall polymers, and other residues from plasma processing. It has been found to leave surfaces free of visual contamination. The process exhibits lower levels of mobile ionic contamination than alternatives. The development of sub-micron devices requires clean via holes for low-resistance contacts. Photoresist stripping methods must address issues like mobile ion contamination and plasma damage while simplifying processes.
IJERA (International journal of Engineering Research and Applications) is International online, ... peer reviewed journal. For more detail or submit your article, please visit www.ijera.com
This document examines the use of complexing agents like EDTA, NTA, IDA, and citric acid to selectively separate Co2+ and Ni2+ ions using cation exchange resins. The key findings are:
1) The presence of complexing agents can significantly enhance the selectivity of Co2+ over Ni2+ by complexing the Ni2+ ions and preventing their exchange onto the resin.
2) The selectivity is strongly dependent on solution pH and the concentration of complexing agent. High selectivity can be achieved at an appropriate pH range and complexing agent concentration.
3) Stronger complexing agents like EDTA and NTA can achieve effective separation at lower pH ranges, while weaker
Sumitomo Metal Mining Co.,- Hydrometallurgical Processing Plant For Low Grade...Archie Casey
The Project is located within the industrial facility of Rio Tuba Nickel Mining Corporation (RTNMC) in Brgy. Rio Tuba, Bataraza, Palawan.
Since 1977, RTNMC has been mining saprolitic nickel ores selling them to ferro-nickel smelters abroad. In more than 25 years of operation, it also generated mine wastes of about 25 million tonnes. Called low grade limonitic mine wastes, these are stockpiled around the mine area.
CBNC will process these stockpiles using the technology called HPAL or high pressure acid leach.
Investigation of the Anodic Dissolution of Zinc in Sodium Chloride Electrolyt...IOSR Journals
The anodic dissolution of zinc electrodes in sodium chloride aqueous solution has been investigated experimentally. The effects of application of polarity reversal (PR), ultrasonic (US) enhancement, stirring, current density (CD), concentration and pH of the supporting electrolyte, and temperature of the bath were studied. The results revealed that application of PR increased the dissolution of Zn but the current was low. However, the application of US enhancement led to higher zinc dissolution accompanied with higher current efficiency (CE). The combination of US enhancement and stirring led to more dissolution of zinc. Increasing the current density and concentration of NaCl increased the dissolution of zinc and the current efficiency was almost constant. On the other hand, pH of the bath did not play a significant effect on the amount of the dissolved zinc or current efficiency. It was also observed that increasing the temperature from 10 oC to 40 oC led to a significant increase in the mass of the dissolved zinc and CE; but the increase of temperature from 40 oC to 50 or 60 oC, however, did not have a significant effect
Synthesis, Spectroscopic Studies and Antibacterial Activity of Novel Schiff B...IRJET Journal
The document describes the synthesis and characterization of novel Schiff base metal complexes derived from condensation of 5-bromosalicylaldehyde, 4,5-dichloro-o-phenylenediamine, and pentane-2,4-dione. Specifically, copper(II), nickel(II), and oxovanadium(IV) complexes were synthesized and characterized using analytical, spectral, electrochemical, and antimicrobial methods. The complexes were found to have general formula [M(L)]X where M is the metal and L is the tetradentate Schiff base ligand. Spectroscopic data indicated the ligand coordinates through the hydroxyl oxygen and azomethine nitrogen. The metal complexes
The document summarizes research on LiMn2O4 cathode material for lithium-ion batteries. It describes the spinel crystal structure of LiMn2O4 and discusses synthesis using solid state combustion with oxalic acid. Characterization with XRD and SEM showed that adding 5 wt% oxalic acid produced smaller, more homogeneous particles. Electrochemical analysis indicated 5 wt% oxalic acid yielded the highest initial capacity of 108.5 mAh/g. Cyclic voltammograms and charge-discharge curves demonstrated better reversibility and electrochemical activity for the 5 wt% sample. The research suggests surface modification could further improve performance of the LiMn2O4 material.
GFS Chemicals has expertise in manufacturing specialty chemicals through its acquisition of Farchan Laboratories. Farchan produces a wide range of acetylenic, olefinic, and silyl intermediates using innovative liquid ammonia and Grignard reaction technologies. GFS offers over 600 acetylenic products, more than any other supplier, and the Farchan acquisition expanded GFS's product catalog and production capabilities for these specialty intermediates.
This document discusses the effects of hydrogen on tantalum and niobium materials. Small amounts of hydrogen can be absorbed by these metals, but higher levels of hydrogen absorption can lead to embrittlement and loss of ductility. The presence of hydrogen is one of the main failure mechanisms for tantalum and niobium in corrosive environments. Several methods are discussed for preventing and detecting hydrogen embrittlement in tantalum and niobium, including controlling temperatures and concentrations, using isolation kits, vacuum degassing, visual inspection of fractures, and resistivity testing. Laboratory corrosion tests were able to predict failure times of tantalum and niobium alloys in sulfuric acid environments.
Managing Mercury in Hydrocarbon Processing Plants During TurnaroundsISCT GROUP US LLC
One of the first works Dr. Roberto Lopez Garcia (aka one of the biggest brains in this business and good friend) and I collaborate on to bring this issue to light in the US and globally. Since this early publication the complicated issues associated with mercury in processing has increased throughout the US as the shale gas plays have developed and refineries have increased their feeds from these plays. In addition the approval of Keystone which takes crude form the oil sands in Alberta (full of metals including Hg) will only compound the mercury issues at US refineries taking this production. Dilution with Bakken production is not really going to eliminate this problem.
The document summarizes Glacius' proposal for a novel waste minimization process for a steel manufacturing plant. The proposal involves utilizing steel slag and waste pickle liquor to produce de-icing fluid. Key aspects of the proposal include a reactor design for the chemical reactions, settling ponds and reservoirs for storage, and an economic analysis projecting a payback period of 6 years and net present value of $24.7 million. The proposal aims to both maximize waste utilization and reduce waste management costs for the steel mill.
This document investigates the use of multi-walled carbon nanotubes (MWCNTs) and MWCNTs with carboxyl content (MWCNT-COOH) to absorb lead and cadmium ions from wastewater. Experiments were conducted with different initial metal ion concentrations to determine absorption rates and capacities. MWCNT-COOH showed higher absorption rates and capacities than plain MWCNTs. Absorption increased with higher initial metal ion concentrations. Data was analyzed using Langmuir and Freundlich isotherm models to determine the best model for describing absorption. The Langmuir model showed better fit for the absorption of metal ions by MWCNTs.
This document summarizes various methods for remediating cyanide contamination. It discusses separation methods like physical separation using membranes or electrowinning. It also discusses destruction methods like oxidation which break the carbon-nitrogen triple bond in cyanide. Common oxidation methods mentioned are acidification/volatilization, which lowers the pH to release hydrogen cyanide gas, and metal addition processes like the Merrill-Crowe process which precipitate metals to remove cyanide from solution. The document provides examples of industrial cyanide remediation processes and compares their effectiveness at treating different cyanide species.
IRJET- Hardness Removal of Groundwater by using Optimum Lime-Soda ProcessIRJET Journal
The document summarizes a study on removing hardness from groundwater in Surat, India using a lime-soda process. Water samples were collected from four zones in Surat with average hardness of 500 mg/L as CaCO3. Jar tests were conducted with varying dosages of lime and soda ash to determine the optimal dosage. Results showed that increasing lime dosage decreased total hardness concentrations. The pH also increased with higher lime and soda ash dosages. The lime-soda process successfully reduced hardness in the groundwater samples.
1) The document describes a SART plant implemented at a gold heap leach operation in Mexico to address high cyanide consumption from elevated levels of cyanide-soluble base metals.
2) The SART plant was originally designed and built in 2008 to treat 340 m3/hr, but was recently upgraded to treat 525 m3/hr and increase copper recovery from the process.
3) Capital costs for the original 2008 SART plant, excluding engineering and feasibility study costs, totaled $4.5 million including equipment, installation, piping and electrical.
This document provides a summary of Mike Rockandel's qualifications and career history. He has over 40 years of experience in process engineering, including metallurgy, minerals processing, chemicals, and environmental industries. He has worked on projects for Rio Tinto, Baja Mining, Aker Kvaerner, and Rio Tinto Diamonds developing processes for copper, zinc, cobalt, lithium, boron, soda ash, and sodium bicarbonate production. Currently he manages a team of process engineers providing technical support for Rio Tinto Americas operations.
This document summarizes a project at Sohar Aluminium to handle hazardous aluminum dross generated at the casthouse. It discusses how dross is formed, its composition, and initial challenges with accumulation. The project implemented internal dross processing by cooling it with inert gas to stop combustion, then feeding it into the bath plant for separation and metal recovery. These improvements addressed dross issues, reduced waste, and allowed for complete recycling and cost benefits.
This document discusses different types of fluxes used in aluminum casting processes. It describes fluxes as mixtures that facilitate removing impurities from molten aluminum alloys. The main types are covering fluxes to prevent oxidation, cleaning fluxes to remove oxides, drossing fluxes to promote separating trapped aluminum from dross, and degassing fluxes containing chlorine and fluorine salts to remove hydrogen by forming gas bubbles. Each flux is designed for a specific purpose based on its chemical composition and reactions with impurities in the molten alloy.
The document discusses various manufacturing processes for metals, including casting, mechanical processes like forging and rolling, machining processes, consolidation/joining processes, and powder metallurgy. It provides details on the casting process, describing the key steps of mold production, melting, and pouring. It notes advantages of casting include the ability to produce complex shapes with little material waste at low cost, though it produces parts with rough surfaces requiring further machining.
This document discusses the casting procedure and defects in dentistry. It begins with a brief history of casting techniques from the 11th century to present. The basic steps of casting include attaching a sprue former to the wax pattern, investing the pattern in a ring, burnout of the wax, and casting of the alloy. Key aspects covered are types of sprue formers and their attachment, crucible formers, casting rings and liners, and the investing procedure. The goals of investing are to produce an accurate mold with adequate expansion to compensate for casting shrinkage.
IJERA (International journal of Engineering Research and Applications) is International online, ... peer reviewed journal. For more detail or submit your article, please visit www.ijera.com
This document examines the use of complexing agents like EDTA, NTA, IDA, and citric acid to selectively separate Co2+ and Ni2+ ions using cation exchange resins. The key findings are:
1) The presence of complexing agents can significantly enhance the selectivity of Co2+ over Ni2+ by complexing the Ni2+ ions and preventing their exchange onto the resin.
2) The selectivity is strongly dependent on solution pH and the concentration of complexing agent. High selectivity can be achieved at an appropriate pH range and complexing agent concentration.
3) Stronger complexing agents like EDTA and NTA can achieve effective separation at lower pH ranges, while weaker
Sumitomo Metal Mining Co.,- Hydrometallurgical Processing Plant For Low Grade...Archie Casey
The Project is located within the industrial facility of Rio Tuba Nickel Mining Corporation (RTNMC) in Brgy. Rio Tuba, Bataraza, Palawan.
Since 1977, RTNMC has been mining saprolitic nickel ores selling them to ferro-nickel smelters abroad. In more than 25 years of operation, it also generated mine wastes of about 25 million tonnes. Called low grade limonitic mine wastes, these are stockpiled around the mine area.
CBNC will process these stockpiles using the technology called HPAL or high pressure acid leach.
Investigation of the Anodic Dissolution of Zinc in Sodium Chloride Electrolyt...IOSR Journals
The anodic dissolution of zinc electrodes in sodium chloride aqueous solution has been investigated experimentally. The effects of application of polarity reversal (PR), ultrasonic (US) enhancement, stirring, current density (CD), concentration and pH of the supporting electrolyte, and temperature of the bath were studied. The results revealed that application of PR increased the dissolution of Zn but the current was low. However, the application of US enhancement led to higher zinc dissolution accompanied with higher current efficiency (CE). The combination of US enhancement and stirring led to more dissolution of zinc. Increasing the current density and concentration of NaCl increased the dissolution of zinc and the current efficiency was almost constant. On the other hand, pH of the bath did not play a significant effect on the amount of the dissolved zinc or current efficiency. It was also observed that increasing the temperature from 10 oC to 40 oC led to a significant increase in the mass of the dissolved zinc and CE; but the increase of temperature from 40 oC to 50 or 60 oC, however, did not have a significant effect
Synthesis, Spectroscopic Studies and Antibacterial Activity of Novel Schiff B...IRJET Journal
The document describes the synthesis and characterization of novel Schiff base metal complexes derived from condensation of 5-bromosalicylaldehyde, 4,5-dichloro-o-phenylenediamine, and pentane-2,4-dione. Specifically, copper(II), nickel(II), and oxovanadium(IV) complexes were synthesized and characterized using analytical, spectral, electrochemical, and antimicrobial methods. The complexes were found to have general formula [M(L)]X where M is the metal and L is the tetradentate Schiff base ligand. Spectroscopic data indicated the ligand coordinates through the hydroxyl oxygen and azomethine nitrogen. The metal complexes
The document summarizes research on LiMn2O4 cathode material for lithium-ion batteries. It describes the spinel crystal structure of LiMn2O4 and discusses synthesis using solid state combustion with oxalic acid. Characterization with XRD and SEM showed that adding 5 wt% oxalic acid produced smaller, more homogeneous particles. Electrochemical analysis indicated 5 wt% oxalic acid yielded the highest initial capacity of 108.5 mAh/g. Cyclic voltammograms and charge-discharge curves demonstrated better reversibility and electrochemical activity for the 5 wt% sample. The research suggests surface modification could further improve performance of the LiMn2O4 material.
GFS Chemicals has expertise in manufacturing specialty chemicals through its acquisition of Farchan Laboratories. Farchan produces a wide range of acetylenic, olefinic, and silyl intermediates using innovative liquid ammonia and Grignard reaction technologies. GFS offers over 600 acetylenic products, more than any other supplier, and the Farchan acquisition expanded GFS's product catalog and production capabilities for these specialty intermediates.
This document discusses the effects of hydrogen on tantalum and niobium materials. Small amounts of hydrogen can be absorbed by these metals, but higher levels of hydrogen absorption can lead to embrittlement and loss of ductility. The presence of hydrogen is one of the main failure mechanisms for tantalum and niobium in corrosive environments. Several methods are discussed for preventing and detecting hydrogen embrittlement in tantalum and niobium, including controlling temperatures and concentrations, using isolation kits, vacuum degassing, visual inspection of fractures, and resistivity testing. Laboratory corrosion tests were able to predict failure times of tantalum and niobium alloys in sulfuric acid environments.
Managing Mercury in Hydrocarbon Processing Plants During TurnaroundsISCT GROUP US LLC
One of the first works Dr. Roberto Lopez Garcia (aka one of the biggest brains in this business and good friend) and I collaborate on to bring this issue to light in the US and globally. Since this early publication the complicated issues associated with mercury in processing has increased throughout the US as the shale gas plays have developed and refineries have increased their feeds from these plays. In addition the approval of Keystone which takes crude form the oil sands in Alberta (full of metals including Hg) will only compound the mercury issues at US refineries taking this production. Dilution with Bakken production is not really going to eliminate this problem.
The document summarizes Glacius' proposal for a novel waste minimization process for a steel manufacturing plant. The proposal involves utilizing steel slag and waste pickle liquor to produce de-icing fluid. Key aspects of the proposal include a reactor design for the chemical reactions, settling ponds and reservoirs for storage, and an economic analysis projecting a payback period of 6 years and net present value of $24.7 million. The proposal aims to both maximize waste utilization and reduce waste management costs for the steel mill.
This document investigates the use of multi-walled carbon nanotubes (MWCNTs) and MWCNTs with carboxyl content (MWCNT-COOH) to absorb lead and cadmium ions from wastewater. Experiments were conducted with different initial metal ion concentrations to determine absorption rates and capacities. MWCNT-COOH showed higher absorption rates and capacities than plain MWCNTs. Absorption increased with higher initial metal ion concentrations. Data was analyzed using Langmuir and Freundlich isotherm models to determine the best model for describing absorption. The Langmuir model showed better fit for the absorption of metal ions by MWCNTs.
This document summarizes various methods for remediating cyanide contamination. It discusses separation methods like physical separation using membranes or electrowinning. It also discusses destruction methods like oxidation which break the carbon-nitrogen triple bond in cyanide. Common oxidation methods mentioned are acidification/volatilization, which lowers the pH to release hydrogen cyanide gas, and metal addition processes like the Merrill-Crowe process which precipitate metals to remove cyanide from solution. The document provides examples of industrial cyanide remediation processes and compares their effectiveness at treating different cyanide species.
IRJET- Hardness Removal of Groundwater by using Optimum Lime-Soda ProcessIRJET Journal
The document summarizes a study on removing hardness from groundwater in Surat, India using a lime-soda process. Water samples were collected from four zones in Surat with average hardness of 500 mg/L as CaCO3. Jar tests were conducted with varying dosages of lime and soda ash to determine the optimal dosage. Results showed that increasing lime dosage decreased total hardness concentrations. The pH also increased with higher lime and soda ash dosages. The lime-soda process successfully reduced hardness in the groundwater samples.
1) The document describes a SART plant implemented at a gold heap leach operation in Mexico to address high cyanide consumption from elevated levels of cyanide-soluble base metals.
2) The SART plant was originally designed and built in 2008 to treat 340 m3/hr, but was recently upgraded to treat 525 m3/hr and increase copper recovery from the process.
3) Capital costs for the original 2008 SART plant, excluding engineering and feasibility study costs, totaled $4.5 million including equipment, installation, piping and electrical.
This document provides a summary of Mike Rockandel's qualifications and career history. He has over 40 years of experience in process engineering, including metallurgy, minerals processing, chemicals, and environmental industries. He has worked on projects for Rio Tinto, Baja Mining, Aker Kvaerner, and Rio Tinto Diamonds developing processes for copper, zinc, cobalt, lithium, boron, soda ash, and sodium bicarbonate production. Currently he manages a team of process engineers providing technical support for Rio Tinto Americas operations.
This document summarizes a project at Sohar Aluminium to handle hazardous aluminum dross generated at the casthouse. It discusses how dross is formed, its composition, and initial challenges with accumulation. The project implemented internal dross processing by cooling it with inert gas to stop combustion, then feeding it into the bath plant for separation and metal recovery. These improvements addressed dross issues, reduced waste, and allowed for complete recycling and cost benefits.
This document discusses different types of fluxes used in aluminum casting processes. It describes fluxes as mixtures that facilitate removing impurities from molten aluminum alloys. The main types are covering fluxes to prevent oxidation, cleaning fluxes to remove oxides, drossing fluxes to promote separating trapped aluminum from dross, and degassing fluxes containing chlorine and fluorine salts to remove hydrogen by forming gas bubbles. Each flux is designed for a specific purpose based on its chemical composition and reactions with impurities in the molten alloy.
The document discusses various manufacturing processes for metals, including casting, mechanical processes like forging and rolling, machining processes, consolidation/joining processes, and powder metallurgy. It provides details on the casting process, describing the key steps of mold production, melting, and pouring. It notes advantages of casting include the ability to produce complex shapes with little material waste at low cost, though it produces parts with rough surfaces requiring further machining.
This document discusses the casting procedure and defects in dentistry. It begins with a brief history of casting techniques from the 11th century to present. The basic steps of casting include attaching a sprue former to the wax pattern, investing the pattern in a ring, burnout of the wax, and casting of the alloy. Key aspects covered are types of sprue formers and their attachment, crucible formers, casting rings and liners, and the investing procedure. The goals of investing are to produce an accurate mold with adequate expansion to compensate for casting shrinkage.
Metal casting involves pouring liquid metal into a mold to produce parts of a desired shape. The key steps are melting metal to create a liquid, pouring it into a mold to achieve a solid shape as it cools and extracts heat, and then removing the solidified part from the mold. The quality of castings depends on factors like the flow of molten metal into the mold, the solidification and cooling process, and the type of mold material used. Common casting methods include sand casting, die casting, and investment casting.
This document reviews recent developments in melting and refining technologies for high-temperature steels and superalloys. It discusses how primary melting techniques are used to synthesize alloys from raw materials, while secondary processes provide additional refining and control of solidification structure. Various primary and secondary melting processes are compared in terms of their capabilities for composition and purity control and for producing consistent, high quality ingots. The most advanced processes combine multiple steps to achieve stringent requirements for products serving at high temperatures.
ICWES15 -Comparative Absorption of Copper from Synthetic and Real Wastewater ...Engineers Australia
The document summarizes research on using modified montmorillonite clay to adsorb copper ions from wastewater. Sodium-exchanged and acid-modified montmorillonite were tested for copper adsorption and shown to effectively remove copper, with uptake described by Freundlich and Langmuir isotherm models and pseudo-second order kinetics. Adsorption capacity was higher for sodium-exchanged compared to acid-modified clay. Testing on industrial wastewater demonstrated the potential for use in real-world treatment applications.
Screening and extraction of heavy metals from anaerobically digested sewage s...IRJET Journal
This document summarizes a study that investigated screening and extracting heavy metals from anaerobically digested sewage sludge using citric acid. The study characterized the sewage sludge and found heavy metal concentrations of copper, lead, nickel and zinc to be above regulatory standards. It then used a full factorial experimental design to study the effects of pH, hydrogen peroxide dosage, and extraction time on removing the heavy metals. Lead removal was highest at 99.9%, followed by nickel, copper and zinc. Statistical analysis found extraction time and hydrogen peroxide dosage to most significantly impact heavy metal removal efficiency.
IRJET- Comparative Studies on Copper Removal by Sawdust and Iron Oxide Na...IRJET Journal
This document presents a study on the comparative removal of copper using sawdust and iron oxide nanoparticles as adsorbents. Batch experiments were conducted to evaluate the effect of parameters like pH, initial concentration, adsorbent dosage, and contact time on copper removal efficiency. The maximum removal efficiencies achieved were 81.32% for sawdust and 98.02% for iron oxide nanoparticles at pH 6 and an equilibrium time of 100 minutes. Column studies showed maximum removal of 68.82% for sawdust and 92.06% for iron oxide nanoparticles. The iron oxide nanoparticles exhibited better adsorption capacity for copper compared to sawdust. The study provides removal efficiencies of the adsorbents under different conditions
Ferrosilicon productiion and submerged arc furnaceNasser Harby
This document provides an overview of ferrosilicon and submerged arc furnace processes. It begins with an introduction to ferroalloys and their classification. Ferrosilicon is used to introduce silicon into molten metals like steel. Submerged arc furnaces are commonly used for ferroalloy production, with carbon electrodes immersed in the furnace charge. The document discusses the raw materials used, including silicon sources like quartz, carbon sources, and their effects on the process. Particle size and carbon reactivity are important considerations for raw material quality.
Ferrosilicon productiion and submerged arc furnace (1)Nasser Harby
This document provides an overview of ferrosilicon and submerged arc furnace production. It begins with an introduction to ferrosilicon alloys and submerged arc furnaces. It then discusses the raw materials used in the process, including quartz, carbon sources, and iron sources. The document outlines the ferrosilicon production process, including charging, stoking, and the reactions that take place in the furnace. It provides diagrams of a typical furnace setup and the zones within the furnace. The summary provides a high-level view of the key topics covered in the document in 3 sentences or less.
Corrosion Inhibition of Carbon Steel in Chloride and Sulfate SolutionsIJERA Editor
The document discusses corrosion inhibition of carbon steel in chloride and sulfate solutions. It studies using a combination of dichromate, molybdate, and nitrite inhibitors to provide high corrosion inhibition. Testing involved immersing steel coupons in synthetic solutions with chloride and sulfate ions and measuring corrosion rates. Results found that a combination of 1 ppm sodium dichromate, 250 ppm sodium molybdate, and 50 ppm sodium nitrite provided the best corrosion inhibition while meeting environmental regulations. Further testing examined the effects of changing inhibitor concentrations and environmental parameters like chloride concentration, rotation speed, and pH. The inhibitor combination performed well except being sensitive to increases in sulfate concentration.
This document discusses the use of vanadium microalloying in steels produced through thin-slab casting and direct charging processes. It notes that these processes differ from conventional steelmaking in ways like using electric arc furnaces, continuous casting into thin slabs, and directly charging slabs without reheating. These differences impact how elements like nitrogen behave and must be considered. The document focuses on how vanadium and nitrogen interact as alloying elements to strengthen steels for this production method.
IRJET- Electrocoagulation Treatment of Electroplating Industrial EffluentIRJET Journal
The document discusses electrocoagulation treatment of electroplating industrial effluent. Electrocoagulation uses aluminum electrodes connected to a power source, generating aluminum ions and hydroxide ions that remove pollutants from the effluent. The study treated electroplating effluent with high levels of zinc and nickel. Treatment at 4A/m2 current density for 120 minutes reduced zinc levels by 78.9%, but did not significantly reduce nickel levels due to the effluent's low initial pH of 1.7. Increasing pH improved removal of both metals during electrocoagulation treatment.
This document discusses iron carbides and their use in steelmaking. Some key points:
- Iron carbide is produced from iron ore using natural gas and can be used as a premium-quality feedstock for electric arc furnaces and basic oxygen furnaces.
- The process is simple and produces iron carbide, water, and carbon dioxide as byproducts. Iron carbide has benefits for nitrogen control and is easy to inject into furnaces.
- Compared to other iron production methods, iron carbide production has lower carbon emissions and the carbon dioxide byproduct can be more easily captured. Commercial plants have been built that can produce over 1,000 metric tons per day of iron carbide.
Nondestructive Characterization for Metal-Matrix Composite Fabrication.pdfmahmoodkhan77
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NFL Nangal was the first key industry set up by the Government of India utilizing surplus power from the Bhakhra Dam project. It established a fertilizer plant in Nangal in 1961 which initially produced ammonium nitrate and heavy water. The plant later added urea production in 1978 and replaced its electrolysis plant with a new front-end plant in 1990. In-situ metallographic testing is carried out to examine the microstructure of components and determine degradation or abnormalities from operational conditions, using a portable kit.
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1. A TECHNICAL PERSPECTIVE ON MOLTEN ALUMINUM PROCESSING
Peter Waite
Alcan International Limited
Arvida Research and Development Center
Jonquière, Québec, Canada G7S 4K8
Abstract However, notwithstanding recent advances in metal quality, the
cast house metallurgist still faces significant challenges. Metal
In today's context of global competitiveness, all factors related to processing and monitoring costs are significant – available
molten metal treatment which directly or indirectly affect product resources must be used judiciously. Pressure to increase
quality, the environment and processing costs must be optimized. productivity and metal throughput are incessant, while at the same
In this regard, technology and innovation play a decisive role for time, metal quality variation is unacceptable. Environment issues
the development and implementation of the most appropriate must be taken seriously and can limit the metal processing options
molten metal treatment processes and practices. The following that are available.
discussion will review the most recent significant developments in
the field of molten aluminum processing and outline potential Recent progress made in the field of molten metal treatment
areas for improvement. technologies is summarized and future challenges are suggested.
Introduction Overview of Metal Processing Steps
In order to meet the continually increasing product performance Many different metal treatment technologies and practices are
requirements of the world market place, molten metal quality is a available to the cast house metallurgist. The successful
major preoccupation of the cast house. In the context of this implementation and use of these technologies is accomplished
discussion, metal quality refers to the degree to which an only when an appropriate balance is achieved between metal
aluminum alloy is free of the following contaminants: alkalis quality, productivity, cost and the environment. The general
(sodium, calcium, and lithium), non-metallic inclusions, and sequence of molten metal processing steps is shown in Figure 1
dissolved hydrogen. Improvements in metal quality have been and consists of crucible pre-treatment upstream of the furnace,
achieved with the development and implementation of molten furnace processing, and in-line treatment – degassing and
metal treatment technologies during the last 20 years. Advances, filtration. Additionally, the transfer of the liquid metal between
particularly during the last decade, are significant and reflect an each processing step must be given particular attention. It is
improved comprehension of the underlying principles governing generally recognized that as the liquid metal advances towards the
molten metal treatment. ingot, metal treatment operations become increasingly "critical".
2. Electrolytic Cell
Crucible
Pre-treatment
Casting
Casting Furnace Degasser Filter
Melting Furnace
Figure 1: Sequence of Molten Metal Processing Steps.
In the past, process development and optimization efforts focused Motivated by cost reduction or simply by a sometimes limited
on individual metal treatment steps. Semi-empirical methods, availability of good quality clean scrap metal, today's aluminum
requiring little knowledge of the underlying metal treatment recycling plants must have increased flexibility to accept variable
mechanisms, were used to relate process changes to final product scrap quality, and as such, the molten metal treatment system must
performance. This situation was complicated by the low impurity be increasingly robust to handle a higher and fluctuating impurity
concentrations that had to be accurately measured and because the load. Similarly, present trends in aluminum smelter operation
available metal quality measurement techniques, at the time, were include efforts to improve current efficiency and to reduce
costly and often laboratory-based - leading to limited acceptance environmental emissions. This has led to increasingly high
or use by the industry. sodium and/or lithium levels in the primary metal produced.
Consequently, improved molten metal treatment performance in
the cast house is necessary.
Molten Metal Analysis and Control
Control Technologies
Impurities
Quantitative instrumental techniques capable of accurately
The types and sources of impurities present in liquid aluminum, as measuring the extremely low concentrations of the various
well as their detrimental effects on specific products, have been contaminants are presently used throughout the aluminum
reviewed in detail elsewhere(1). It is pertinent to note that the industry.
molten aluminum supplied to the cast house comes from two
distinctly different sources: smelter electrolysis and remelt/recycle Inclusions – Metal Cleanliness Considered industry standards, the
operations. The impurities present in the metal supplied from LiMCA and PoDFA metal cleanliness assessment techniques,
these sources are also different and can affect the metal treatment developed by Alcan, have been previously described in
strategy that is used. Remelted metal is normally associated with detail(2, 3, 4). Briefly, LiMCA is based on the resistive pulse
higher levels of hydrogen, calcium, and hard oxide inclusions that principle and generates both an inclusion concentration value and
are formed during high temperature scrap melting processes. On a complete size distribution. PoDFA is based on the filtration of
the other hand, smelter metal is associated with higher levels of 1-2 kg of metal through a well-calibrated small filtration disk with
sodium, aluminum carbide inclusions, as well as non-metallic subsequent metallographic examination of the inclusion
inclusions generated from the addition of large quantities of concentrate. Information on inclusion species and sizes, as well as
alloying elements. Table I summarizes the impurity levels present a semi-quantitative total inclusion level expressed in mm2/kg are
in the metal supplied to the cast house. obtained. LiMCA and PoDFA are complementary technologies in
as much as their respective quantitative and qualitative capabilities
Table I Typical Impurity Levels in Metal from Smelter and combine to give essential data required for an informed judgment
Remelt Sources of metal cleanliness.
Characteristic Smelter Remelt However, significant challenges remain to be overcome. The
Alloyed or close to LiMCA instrument is on-line, but complex to operate, and PoDFA
Composition ≥ 99.7% Al analysis requires metallographic expertise/facilities and is thus
final composition
off-line. An inherent weakness of the LiMCA technique is the
Hydrogen 0.1 – 0.3 ppm 0.2 – 0.6 ppm inability to distinguish the physical state of the inclusion.
Consequently, and unless a deep bed filter is used, reliable
Alkali Na 30 – 150 ppm ≤ 10 ppm LiMCA measurements are difficult to obtain immediately
Ca 2 – 5 ppm 5 – 40 ppm downstream of an in-line degasser(5) due to the complex
Li 0 – 20 ppm < 1 ppm interactions between the gas/liquid/solid inclusions present.
Exploratory development work on an alternative inclusion
0.5 < mm2/kg < 5.0
Inclusions > 1 mm2/kg detection technology focuses on the use of ultra-sound(6). It
Al2O3, MgO,
(PoDFA scale) Al4C3 remains that a simple, low cost yet quantitatively accurate on-line
MgAl2O4, Al4C3, TiB2
metal cleanliness assessment tool is needed by the industry.
3. Hydrogen The AlSCAN™ technology(7, 8) is now in use through- Molten Metal Processing Technologies
out the industry and is recognized as the standard technique for
on-line hydrogen analysis. Due to it's high precision, AlSCAN Over the last 10 years, the need to produce higher quality products
has made possible the quantification of different phenomena (such has encouraged nearly uninterrupted development efforts in the
as ambient humidity) affecting hydrogen in molten aluminum. field of metal processing technologies. The clear benefits of these
technologies with respect to quality, cost, productivity and the
Chemical Composition Optical emission spectroscopy has environment, has led to their widespread use throughout the
established itself as the reference analysis technique for the aluminum industry.
measurement of alloy chemical composition at the level of major
constituents, as well as trace elements. A complex calibration and To appreciate the overall molten metal processing performance
alloy matrix correction procedure is required for the different alloy that is now demanded in the cast house, Figure 3 summarizes the
families, and remains a technical obstacle to overcome. low impurity levels that must be achieved for various products.
Compared to the incoming impurity levels (Table I), highly
Control Strategies efficient impurity removal is required during metal processing.
Measurement techniques capable of quantifying all aspects of
metal quality have been in widespread use for roughly 10 years.
3
Alkalis
With the specific objective of process development, focused Inclusions Parts per
campaigns in the cast house involving metal quality 1 million
measurements, before and after the different stages of metal 1000
Unfiltered
treatment, have permitted the identification of important process
Hydrogen
parameters. Combined with heightened efforts in metallurgical
Alloy
process modeling, an improved understanding of the underlying 100
Extrusion
Pure
metallurgical principles has been achieved, allowing advances in Parts per
the development and optimization of metal treatment technologies billion
and practices. 10
Filtered
The considerable measurement costs related to these process
Foil
Filtered
development activities were easily justified by the 1
Alloy
Computer
performance/quality improvements that were progressively 1000
obtained. However, at present, molten metal treatment
Disks
technologies have reached a state of maturity that no longer
100 Parts per
requires such a high level of quality measurement support. trillion
The most effective use of metal quality measurement resources is
being re-examined. A strategy focusing on product quality control 10
and process capability monitoring is presently emerging.
Statistical process control techniques are being exploited to Figure 3: Typical Impurity Concentrations in Some Aluminum
maximize the amount of information extracted from the data. The Products.
use of control charts and the establishment of process control
limits enable the metallurgist to learn from the process in order to Crucible Pre-treatment
improve it. Finally, process benchmarking and data exchange
between different divisions of a company facilitates the Several crucible-based treatment technologies(9, 10, 11) have been
establishment of process "best practices". Figure 2 summarizes developed with the objective of removing alkalis and inclusions
this metal analysis and control strategy. from the metal prior to transfer into the casting furnace. All these
technologies are similar in as much as a reactive flux (either
chlorine-based or salt-based) is injected into a well-stirred crucible
MEASURE of liquid aluminum. The present consensus favors the chlorine-
free technology for both performance and environmental reasons.
CONTROL / COMPARE Due to the crucible shape (surface/volume ratio), the metal depth
and the intensity with which the metal is stirred, crucible pre-
treatment is rapid, environmentally sound and significantly
reduces the need for subsequent furnace fluxing.
UNDERSTAND
In the past, crucible pre-treatment technology was applied almost
exclusively to smelter applications. More recently, and as the
IMPROVE performance of subsequent furnace treatment technologies have
improved, the need for crucible pre-treatment has been re-
Figure 2: Metal Quality Measurement and Control Strategy. questioned with respect to its costs versus its advantages.
However, in the present context of increasing alkali impurity
levels in primary smelter metal, and the need to accept potentially
lower quality scrap in recycling operations, the beneficial impact
4. of crucible pre-treatment can only become more significant for cleanliness, alkali removal, as well as dross formation, have been
both smelter and recycle-based cast houses. Clearly, the challenge quantified for a wide variety of alloys. In the past, limited
is to readily identify situations where the benefits of crucible pre- improvements to lance fluxing were achieved simply by the use of
treatment can be best exploited. With more widespread use more lances or by the introduction of porous plugs (with the
envisioned, molten metal management may also become an issue. associated operational difficulties).
Finally, extension of this concept to include alloy preparation has
the proven potential(12) for further increasing the value of this Recent improvement to furnace treatment effectiveness has been
metal processing step. achieved by "process intensification" aimed at increasing metal
stirring and fluxing kinetics. Metallurgical modeling has
Furnace Treatment confirmed(19) that the rate limiting step of the furnace fluxing
process, assuming the presence of a minimum of bulk metal
The most common type of casting furnace in current use circulation, is the gas/liquid interfacial contact area generated by
throughout the aluminum industry is the fossil fuel heated the gas purging system.
reverberatory design. The reverberatory furnace, containing a
relatively shallow melt depth, with a high surface area to volume The rotary gas injection (RGI) furnace fluxing technology,(20, 21, 22)
ratio, is optimized for heat transfer. This melt geometry, utilizing high shear gas dispersers, has been know for some time.
combined with the lack of bulk metal circulation, does not This furnace fluxing technology, and others(23), markedly
promote efficient metallurgical treatment. In addition, the vertical increases the interfacial contact area between the liquid metal and
temperature gradient that is generally established through the melt the fluxing agent. Recent adaptation of this technology by the
can be greater than 200oC and is responsible for elevated dross aluminum industry has resulted in significant gains in the cast
formation and reduced heat transfer. These problems are house. Increased impurity removal rates have reduced furnace
magnified as furnace sizes constantly increase. cycle times and improved productivity. The absolute metal
quality levels achieved have improved, lessening the load on
Conventional furnace fluxing with static lances is generally subsequent in-line metal processing steps. Equally as important,
accepted as a rather inefficient way to treat molten aluminum, and significant reductions in chlorine consumption, made possible by
depending on the metal quality requirement, excessively long the improved process efficiency, have had a direct and positive
treatment periods are necessary. This has a negative impact on impact on atmospheric emissions.
both productivity and the environment.
Salt fluxes can be used effectively for the replacement of chlorine
In an effort to overcome reverberatory furnace design limitations, during furnace fluxing(24). Rotary flux injection technologies have
considerable effort has been invested by the aluminum industry to also provided the opportunity to replace chlorine with a salt-based
understand the fundamental metallurgical phenomena taking flux(25, 26) while reducing environmental emissions and
place(13, 14, 15, 16) and to apply this understanding to improve maintaining metallurgical treatment performances comparable to
processing technology and practices. During the last decade, two chlorine. Figure 4 shows the impact of these advances on the
methodologies have been pursued to overcome the inherent overall chlorine consumption of a cast house.
inefficiencies of furnace treatment: first, by directly improving
the efficiency of furnace treatment itself, and secondly, by
reducing the need for furnace treatment and exploiting the more 0.3 - 0.7
Kg/t
efficient crucible pre-treatment and/or in-line treatment
technologies. 0.1 - 0.2
Kg/t
Stirring In the past, stirring by lance gas injection was
0.05
commonplace and suffered from limited effectiveness as well as Kg/t
increased dross generation. Today, advanced subsurface stirring 0
Kg/t
technologies include: pneumatic jet stirring, electromagnetic
approaches and rotary devices.
The metallurgical and operational advantages of forced metal Lance
circulation have been previously reported in detail(17) and include Furnace (Chlorine) RGI RFI
Fluxing (Chlorine) (Salt)
rapid homogenization of the alloy, reduction of the temperature Target
Ò0Ó
gradient and the associated metal oxidation, increased uniformity In-Line Chlorine Chlorine
Chlorine
and consistency of metal processing and improvements to furnace Fluxing Chlorine
control in general. The use of bulk metal circulation systems has
grown throughout the industry.
Figure 4: Progressive Reduction of Chlorine Consumption in the
Fluxing Furnace "fluxing" refers to the removal and separation of Cast House.
impurities from liquid metal by direct reaction and dewetting
based on the use of a chemically active agent. Until recently, the However, there remain important challenges to overcome with
aluminum industry relied exclusively on the use of chlorine for respect to furnace treatment. The casting furnace is not an
fluxing. efficient chemical reactor. Although present design limitations
have been partially overcome by the introduction of improved
The complex mechanisms of furnace fluxing with static lances and fluxing technologies, furnace fluxing cannot provide metal that
chlorine have been studied in detail(18) and its effects on metal meets the cleanliness requirements of critical products.
5. Subsequent in-line metal processing is still necessary. There is a the unit between casts and the resulting metal loss at alloy change.
general need to reduce metal surface turbulence in the furnace that The large floor area requirement and equipment complexity is also
leads to dross formation and metal loss. The majority of dross is becoming a very important issue for the cast shop.
generated during metal transfer into the furnace, with the
remaining dross generated during other furnace processing To address these issues, a recent in-line degassing innovation is
activities, including alloy addition and skimming. Employing the the development of a trough-based process(31, 32, 33) targeting multi-
best technologies available today, including siphon metal transfer, alloy cast houses. The trough-based process virtually eliminates
a target dross generation rate of approximately 1% is possible. metal loss at alloy change and maintains roughly equivalent metal
However, siphoning cannot be used in all cast houses, thus treatment performances and capacities. Development of the Alcan
underlining the need for continued efforts in the area of furnace Compact Degasser technology in particular, was based on the use
design for improved metal transfer. Finally, the trend towards of a hydrogen diffusion model(34) and is a prime example of how a
casting furnaces with greatly increased capacities severely limits fundamental understanding of the metallurgical principles can lead
production flexibility with respect to batch size and alloy change. to process innovation.
In-line Metal Treatment The use of high shear rotary injectors with chlorine-containing gas
mixtures for the treatment of Al-Mg alloys leads to the formation
Due to the inherent inefficiencies of furnace treatment, a growing of minute magnesium chloride inclusions. If an effective metal
emphasis has been placed on the utilization of in-line metal filtration system is not used, the entrainment of these inclusions
processing over the last 20 years. Many in-line treatment downstream of the degassing unit tends to accelerate surface
processes have been developed with the objective of providing oxidation of the molten metal. Oxide-related production or ingot
more efficient and consistent metal treatment performance, while quality problems can result. This phenomenon can limit the
reducing treatment time, emissions and metal loss due to dross amount of chlorine that can be used during in-line degassing, the
formation. There are two categories of in-line metal treatment consequence of which is poor alkali removal performance. Work
processes namely, degassing/fluxing and filtration. has been initiated on separation techniques for the removal of
chloride inclusions(35, 36) in an effort to overcome this limitation.
Degassing The in-line degassing process is now widely accepted
and used almost universally throughout the aluminum industry. The elimination of chlorine from the cast house is advantageous
During the degassing treatment, a gas composed of argon and for safety and environmental reasons, as well as for reduction of
chlorine is dispersed into the liquid metal using one or more high- maintenance costs. Proven alternatives to the use of chlorine exist
speed rotary injectors. The in-line degassing process design is for both crucible pre-treatment and furnace fluxing. Using these
based on the classic multi-stage stirred tank reactor and on salt-based alternatives, the overall chlorine consumption in the
recognition of the need to generate small gas bubbles to increase cast house can be drastically reduced without penalizing metal
the interfacial gas-metal contact area. Due to their functional quality or productivity. The last technical barrier to a truly
similarity, all rotary-type in-line fluxing processes provide chlorine-free cast house is the development of a chlorine
roughly equivalent metal treatment performance. It should be alternative for in-line degassing. However, no such chlorine
noted that although these processes are called "degassers", they alternative presently exists. Today, the only option is to operate
function to remove not only hydrogen but inclusions and alkali the degasser without chlorine while accepting reduced
impurities as well. The physical and chemical factors which metallurgical performance - albeit at the same time, solving the
influence in-line degassing/fluxing performance have been magnesium chloride entrainment problem. In this context, and
published in detail elsewhere.(27, 28) keeping in mind the integrated approach to metal treatment, zero
chlorine operation for in-line degassing is a potentially viable
Recent advances in the design of in-line degassers have resulted in solution for achieving a chlorine-free cast house. Upstream and
more efficient and consistent metallurgical performance. downstream processing practices/technologies would have to be
Improved rotary gas dispersers with increased shearing(29) altered to maintain the overall metal treatment performance of the
maximize gas-metal contact area – a necessary condition for system.
efficient metal treatment.
Tighter environmental emission limits are issues that must be
The capacity of in-line degassing technologies has been scaled up addressed. Will technological improvements or operational
by the use of multiple staging, in order to meet the demands of changes be sufficient to meet the environmental regulations of the
increased casting rates. Multiple staging also has the advantage of future? Perhaps a more drastic re-thinking of the in-line degassing
having "built-in redundancy". The impact of a rotor failure on the process will be required.
metal quality is less severe. Another recent improvement is the
operation of in-line degassers in a "sealed" mode,(30) that is to say, Filtration In the aluminum industry, molten metal filtration has
with an inert cover gas – essentially free of oxygen – over the been used in one form or another for many years(37). It is common
liquid metal surface inside the unit. The impact of this to use a filter strictly for precautionary reasons, that is to say, as a
development on the removal of impurities has not been fully "safety net" to guard against uncontrolled upstream process
quantified. However, there are definite advantages in terms of variations that result in sporadically high inclusion levels.
considerably reduced dross generation, easier operation However, in the context of this discussion, the use of a filter is
(skimming less frequently) and possibly lower particulate considered an essential metal processing step. The objective of
emission rates. filtration is to improve the metal quality to the degree required for
demanding products/applications.
On the other hand, scale-up of the conventional multiple-stage
degasser has greatly increased the amount of metal retained inside
6. Unfortunately, a poor scientific understanding of the fundamental necessary to filter hundreds or thousands of tons of metal between
mechanisms taking place during aluminum filtration has hampered media changeover. The large flow area of these filters reduces the
developments in filter design. Empirical design methods are often metal velocity and greatly improves the filtration efficiency at the
used based on trial and error. The filter was considered a "black expense of a high metal holdup volume and a high floor space
box" because it was almost impossible to obtain a direct measure requirement. The elevated cost associated with filter media
of what the filter was doing. At best, physical model analogues changeover limits the use of multi-cast filters to cast houses
(water models) were used as a design guide. having infrequent alloy changes.
Two technical advances have started to change this situation. Regardless of whether a deep bed filter, a ceramic foam filter
First, is the development of inclusion measurement capabilities. (CFF), or a cartridge filter is used, the technical challenge facing
For example, the use of LiMCA to quantitatively measure metal metal filtration has always been defining the optimum balance
cleanliness has resulted in a practical comprehension of filter between the required metal cleanliness, the filtration cost, the
behavior in terms of operational phenomena such as inclusion available head loss and more recently with significantly increased
release events, maximum filter loading and the impact of metal casting rates, the size of the filter.
velocity on filtration efficiency. Secondly, and more recently, is
the scientific advancement in fundamental research that has There is a definite need to develop an efficient, low hold-up
started to elucidate the important mechanisms that are active filtration process capable of treating high metal flow rates.
during aluminum filtration.(38, 39, 40) However, continued effort is
required to gain a more complete understanding of depth filtration, Metal Conveying
the knowledge of which can eventually serve as the basis for more
sophisticated filter design techniques. Particular attention must be given to the metal transfer equipment
that connects the elements of an integrated metal treatment
What is understood today? Filtering techniques employed in the system. Metal turbulence and cascading must be avoided. The
aluminum industry are mostly based on the depth filtration mode resulting oxides that are formed can undo much of the metal
which involves the deposition and retention of inclusions cleanliness gains that were achieved during upstream processing.
throughout the entire depth of the filter. Inclusions are removed In addition, it is recognized that the refractory and patching
from the metal stream by sedimentation and are very weakly materials used in troughs (and in-line treatment units) can lead to
retained on the surface of the filter medium. Filtration the formation of heterogeneous inclusions. If this occurs late in
performance is improved by: the sequence of metal processing, the effects could be highly
detrimental on product quality. Even ambient humidity can cause
providing a stable and wetted interfacial contact between problems and has been shown to cause hydrogen pick-up in liquid
the liquid metal and the filter medium; metal exposed to air. Under conditions of high ambient humidity,
reducing pore size; products with strict hydrogen limits can only be cast with great
increasing filter depth; difficulty.
reducing the metal flow velocity.
The basic trough design has not changed appreciably for decades.
A major constraint of aluminum filter design is the operational Unlike the magnesium industry, where elimination of the metal
limitation of the very low head loss that can be accepted across the free-surface has been accomplished using closed liquid metal
filter(41). Note that the factors that improve filtration performance conveying systems, the reactive/aggressive nature of liquid
(above) all tend to either increase the head loss or increase the aluminum has prevented equivalent developments in this industry.
filter size – both of which are undesirable. Finally, more work is Upon completion of metal processing, there is a need to maintain
needed to relate molten metal cleanliness to product properties and the liquid metal at its highest quality level for delivery to the
performance. In many cases, the real metal cleanliness level that casting machine. The present trough design cannot always fulfil
is needed for a particular product is not properly quantified. this requirement.
Note that cake mode filtration is not presently used in the Future Implications
aluminum industry. Cake filtration involves the deposition of a
layer of inclusions at the inlet to the filter medium with little or no The integrated approach to metal treatment that has just been
penetration of the inclusions into the internal pore structure of the described has gone through a period of process development and
filter. This results in a very rapid metallostatic head build-up and optimization. Each element of the treatment sequence is being
is unacceptable for cost and practical operating reasons. pushed to its maximum. Although there remain challenges, only
step-wise improvements to quality/productivity/capacity are
Single-use filters such as the ceramic foam filter (CFF) are anticipated.
physically small and are changed after every cast. This gives the
advantage of low floor space and low metal holdup - facilitating In order to make a "quantum step" change, future technical
alloy changes. However, because of their relatively small hurdles may best be overcome by a complete re-thinking of the
dimensions and the high metal velocity through the filter, molten metal treatment strategy in the cast house. It must be
metallostatic head loss considerations limit the thickness and the recognized that multiple interventions are presently required to
minimum practical filter pore size that can be used. As a remove some impurities. For example, it is necessary to use all
consequence, these filters are not highly efficient(42). the metal processing steps to remove non-metallic inclusions,
while alkali removal is done during two or three steps. The future
On the other hand, deep bed filters are used during multiple casts. challenge may be to re-think metal treatment technologies,
They are physically large to contain the amount of filter media including the casting furnace, starting from a "carte blanche" - the
7. premise being that a metal processing step should be done once, 3) J.-P. Martin, R. Hachey, and F. Painchaud, "On-line Metal
but it must be done "right". For example, if inclusion-free metal Cleanliness Determination in Molten Aluminum Alloys Using
could be produced in the casting furnace, in-line treatment for the LiMCA II Analyser" Light Metals, 1994, 915-920.
inclusion removal would no longer be necessary. Conversely, if a
"super" filter could be developed capable of accepting very high 4) D. Doutre et al., "Aluminium Cleanliness Monitoring:
inclusion loading, upstream metal processing for inclusion Methods and Applications in Process Development and
removal would no longer be necessary and significant productivity Quality Control", Light Metals 1985, TMS-AIME, 1179-1195.
gains and/or processing cost reductions could be achieved. 5) H. P. Krug, and W. Schneider, "A Contribution to Inclusion
Measurement After In-line Degassers with PoDFA and
LiMCA", Light Metals, 1998, 863-870.
Conclusions
6) I. D. Sommerville, N. D. G. Mountford, and L. C. B. Martins,
There still remain key molten metal treatment challenges in the "Laboratory and Industrial Validation of an Ultrasonic Sensor
cast house. for Cleanliness Measurement in Liquid Metals", Light Metal,
2000, 721-726.
Molten metal processing must be more robust – capable of 7) J.-P. Martin, F. Tremblay, and G. Dubé, "Alscan: A New and
accepting poorer quality metal at the input, while producing Simple Technique for In-line Analysis of Hydrogen in
higher and less variation metal quality at the output. Aluminum Alloys", Light Metals, 1989, 903-912.
There is a need to develop a more selective on-line inclusion 8) C. Dupuis et al., "An Analysis of Factors Affecting the
detector. Response of Hydrogen Determination Techniques for
Aluminum Alloys", Light Metals, 1992, 1055-1067.
Further development is needed to optimize furnace design
with respect to processing performance and batch size 9) G. Dubé, and V. J. Newberry, "TAC – A Novel Process for the
flexibility. Removal of Lithium and Other Alkalis in Primary
Aluminum", Light Metals, 1983, 991-1003.
The last technical barrier to a truly chlorine-free cast house is
the development of a chlorine alternative for in-line 10) B. Rasch, E. Myrbostad, and K. Hafsas, "Refining of Potroom
degassing. Metal Using the Hydro RAM Crucible Fluxing Process", Light
Metals, 1998, 851-854.
Continued effort is required to gain a more complete
understanding of depth filtration mechanisms. 11) F. Achard, and C. Leroy, "Pre-treatment in Potlines Crucibles:
The Mixal Process", Light Metals, 1990, 765-768.
More work is needed to relate metal cleanliness requirements
to product properties and performance. 12) B. Gariépy et al., "Aluminum Ladle Metallurgy (ALM): A
New Process for More Efficient Alloy Preparation", Light
The development of an efficient, low holdup filtration Metals, 1988, 457-462.
process capable of treating high metal flow rates is needed.
13) B. Kulunk and R. Guthrie, "On the Kinetics of Removal of
Improvements are needed for liquid metal conveying systems Sodium from Aluminum and Aluminum-Magnesium Alloys",
to prevent dross formation and metal loss. Light Metals, 1992, 963-975.
14) G. K. Sigworth, "Gas Fluxing of Molten Aluminum", Light
Acknowledgements Metals, 2000, 773-778.
15) R. R. Roy, T. A. Utigard, and C. Dupuis, "Inclusion Removal
The author wishes to thank Alcan International Limited for the During Chlorine Fluxing of Aluminum Alloys", Light Metals,
permission to publish this article. Discussions and suggestions 1998, 871-875.
during the preparation of this article, made by Messrs. Ghyslain
Dubé, Claude Dupuis and Dr. Jean-Pierre Martin, are also 16) R. R. Roy, T. A. Utigard, and C. Dupuis, "Inclusion Removal
gratefully acknowledged. Kinetics During Chlorine Fluxing of Molten Aluminum",
Light Metals, 2001, 991-997.
17) M. A. Thibault, J. C. Pomerleau, and F. Tremblay, "Molten
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